Reducing zinciferous materials



May 7, 1929 F. G. BREYER ET A1.

REDUCING ZINGIFEROUS MATERIALS 6 Sheets-Sheet Filed April 20. 1927 @M w I W i f ATTORNEYS xNvENToRS G fw w 151% A uw l .l,

May 7, 1929.

E G. BREYER ET A1,V

REDUCING ZINCIFEROUS MATERIALS Filed April 2b, 1927 :e sheets-sheet 2 INVENTOR May 7, 1929 F, G. BRI-:YER ET A1. y 1,712,134

REDUCING ZINCFEROUS MATERIALS Filed April 20, 1927 e snee eet 3` INVENTORS M r ATTORNEYS May 7, 1929- E G. BREYER ET AL '1,712,134

REDUG ING Z INC IFEROUS MATERIALS` Filed April zo, 1927 e sheets-sheet' 4 May 7, 1929-- F. G. BREYER ET A1.

REDUCING. ZINCIFEROUS MATERIALS* Filed April 20, 1927 6 shee1s;shee1 5 INVENTORS fwd G.,

v uw' f *I4/HL f WJ@ ATTORNEYS May 7, 1929- F. G. BREYER ET AL REDCING ZINCIFERoUs MATERIALS Filed April zo, i927 6 Sheets-Sheet 6 `INVENTORS G @a M ATTORNEYS Patented May .UNITED- :sr

'Aras rari-:Nr oFF-ics.y

'FRANRd Bnnxnn AND EARL n. BUNcE, or -rALiriiRrom ,PENNSYLVANIL "assicNoRs 'Y To 'THE NEW JERSEY -ziNc COMPANY,

'NEW cansar".

obs-,NEW YoRx, N. Y., A coRroRii'rioN or REDucINe ziNcirERoUs MATERIALS.

Application ledrprilgflg?. Serial No. 185,331.

This invention relatesto1 the reducing'ifor "sineltingf ofzinciterous materials and has for` its object-the provision of 'certain improvements' in the reduction or smelting of such materials. i The invention aims particularly to provide a new method of reducing or sinelting zincii'erous materials in Which very substantially larger charges may be more economically Worked with substantially .increased extraction oi zinc and With increased recoveries 'of commercially marketable forms ot Izinc., than in the heretofore customary practices of commercial'zinc smelting. A. further object of the invention isto provide a commercially economical and practical method of reducing or smelting zinciferous material-fin a substantially horizontal and externally heated iceducing chamber, preferably in a substantially continuous manner, and on a relatively large ln our copending patent application,

scale and-in which there is produced -metallic zinc vapor ca-pable of being directly and economically condensed to zinc metal. Another object of the invention is the provision of an improved zinc smelting apparatus or furnace having a substantially horizontal and externally heatedl reducing chamber through vxv vhich the charge undergoing reduction is pro gressively advanced.A

Serial No.' 163,902, filed January 27, 1927, We have described an improved method of reducing a porous charge of agglomerates of mixed zincp v iferous andreducing materials in which the transfer. of heatthrough the charge is eftected iny large part by currents oi? hot gases flowing through the voids of the charge. In one of its aspccts,the present invention involves the practice o the invention lof that -applicationv in a substantially horizontal and externally heated reducing chamber through `which the'porous charge progressively passes.

- In another aspect,

the invention contemplates progressively passing a porous charge of agglomedrates of -mixed zinciferous and reducing materials through a substantially horizontal and externally heated reducing chamber unidei"v conditions substantially avoiding relative movement 4of the individual agglomerates,

and in the course of such passage heating the' charge to a suiliciently high temperature'to `reduce the compounds of zinc and volatilize the resulting metallic zinc, preferably Iwithout slagging or fusing the charge. The resulting Ifmetallic zincvapor is withdrawn from the reducing chamber and' may advantageously be condensed to zinc metal. The porous ,charge ot agglomeraties of mixed zinciferous 'material and carbonaceous reducing agent may b e supported, in its passage through the reducing chamber, on a traveling hearth, or the like. ,lt is our preferred practice to support the porous charge on abed of lines carrie-d bya traveling conveyor moving through the reducing chamber and, in effect, constitilting the bottom thereof.,l lWhile the invention may be used for the production of any ot' the usual commercial products obtained in zinc smelting, such as-spelter, zinc oxide, zinc dust or blue povvder,'it is of special advantage when used or the production of zinc y'metal or spelter. iv i In practicing the imethod of zinc smelting described in our aforementioned application, it is important that the agglomeraties constituting the porous charge should not, in their passage through the reducing chamber, break dovvnv or sand and thereby choke or lill the voids between the agglomerates to .an objectionable extent, since these voids constitute the heat-carrying gas passages upon which depends the efficacy f the process for Llarge,

`of coherence between the particles of ore and l reducing agent, thus making-them more or less readily friable or possessed of a sanding tendency. This tenderness or sanding tendency is affected by the nature of the ore, the nature of the reducing agent, and the nature of any reduction activators present, as well as by the bonding agency that holds together the relatively small particlescomposingthe agglomcrate. It is also affected by the way in which the bond has been established, as well as bythe rate at which the agglomerates are heated in the reducing chamber.

When the particles of the agglomerate are bonded together with a caking material like bituminous coal, sanding difficulties may be ica` sanding: difficulty is encou'n e tendency to destroy a 11,0

ores, reducing agents, reduction activators and' bonding agencies, as Well as the greatest freedom 1n thev heating up of the charge 1n the reducing chamber, it is important that the agglomerates be furnaced with as little shearing or abrading stress between the agglomerates as possible. This requirement of minimum abrading and shearing stresses between the agglomerates of a porous Vchargev is not easily satisfied Where at the same time it is required that the porous charge be progressively passed through the reducing chamber.

The method of our present invention, in

Which the porous charge of agglomerates is progressively advanced through a substantially horizontal reducing chamber While supported in a relatively quiescent condition on a traveling hearth, admirably satisfies the charge progression demand, and at the same time permits the use of the greatestV variety of ores, reducing agents, reduction activators, and bonding agencies, Without danger of impairing the desired porosity of the charge during furnacing. In the methodof the invention, the agglomerates are progressed 'or advanced through the reducing chamber With substantially no attrition one upon the other and With only the sidewall abrasion to produce void-filling fines. The Wider a vfurnace for any given charge,.the less important this side Wall abrasion becomes.

The passage of the porous charge of agglomerates through the reducing chamber under conditions substantially avoiding relative movement of the individual agglomcrates is, therefore, one of the characterist-ie features of our invention. In accordance With this aspect Vof the invention, the porous chargeofagglomerates is progressively passed through the reducing chamber Without substantial breaking down of the agglomerates and without substantial relative movement of the individual agglomerates during such passage. By relative movement of individual agglomerates in a porous charge of agglomerates, we mean either translatory movement or rotary movement, or both, of one or more agglomerates with respect to any other agglomerate or agglomerates in the charge whereby abrading and rupturing stresses are imposed upon the agglomerates. By avoiding such relative movement of individual agglomerates in their passage through erates of orc and caking coal mixed with an appropriate reduction activator such as sodium carbonate. The reduction activator has a pronounced tendency to make the agglomerates tender and liable to sand under the conditions encountered in the reducing chamber. Such agglomerates, after caking at approximately 700 C., are relatively strong and may be transferred red hot from the caking furnace to the charging endof the horizontal reducing chamber Without substantial fracturing or sanding. lVhen, however,such agglomerates are passed through the reducing chamber, and especially after a considerable proportion of their zinc con' tent has been distilled off, they become relatively tender. By the method ofthe invention, such agglomerates are carried through the reducing chamber substantially in the same physical size and shape as they enter the reducing chamber from the charging hopper.

In addition to insuring the passage of the agglomerates through the reducing chamber without abrading and rupturing stresses, the method of the invention prevents packing of the agglomerates due to their jostling and settling together. 'Such packing of the agglomerates tends to reduce the porosity of the charge and thereby reduces the rate at which heat can be transferred to those por tions of the charge remote from the heated Wall of the reducing chamber.

The costs of agglomerating and handling the agglomerates through dryers, caking apparatus, deoxidizers, and the like, preceding the introduction of the agglomerates into the reducing chamber, constitute a very substantial proportion of the total costs of the reducing operation. The method of the invention makes possible very substantial economies in the costs of handling the agglomerates. Thus, when agglomerating by briquetting, a traveling hearth or pan conveyor serves as an excellent lreceiver for briquettes discharged from a briquetting press, and when this traveling hearth or pan conveyor serves at the same time to support the briquettes in their passage through dryers, caking apparatus, or other auxiliaries, as Well asthrough the reducing chamber, ver)l important economies are realized in the opertion, the furnace structure, auxiliaries, re-

cuperator, deoxidizer, and other appurtenances may be built on ground level foundations in convenient relation with one another. Certain economies in the construction, operation and maintenance costs ofthe furnace thus become possible, as compared with furnaces in which the reducing chamber is in an upright or vertical position. In the present invention, all of the charge end auX- iliaries, such as agglomerating apparatus, dryers, caking apparatus, etc., can be on the ground level, ariel` whatever attention these auxiliaries, or other appurtenances of the furnace, require can be more readily and economically provided than in the case of an apparatus having the auxiliaries or appurtenances on dierent levels.

When anthracite fines or anthracite dust coal is used as the reducing agent and the agglomerates are made by briquetting and bond- .ing together the relatively fine ore and coal by means of dried sulite liquor, the drying 1 "A anddeoxidizing chamber may advantageously be an extension of the reducing chamber Si in advance of the'zone where the first zinc4 sa. laden gases aretaken ofto the condensers.

y,When a recuperator is included in the appa-- ratus, the drying and deoxidizing chamber may be externally heated by the gases exiting from the recuperator, which gases would otherwise go direct to a stack. -If desired, the recuperator exit gases may be passed directly over or through the agglomerates in the drying and deoxidizing chamber. The gases from the deoxidizing chamber, particularly when bituminous coal is used as a caking` and/or reducing agent, may be blown or y drawn into the fuel gasmain of the recuperator and utilized in the'firing of the heating flue of the reducing chamber. With such an arrangement of apparatus', a briquetting press may advantageousl ybeso positioned as to feed the briquettes iseharging therefrom to the front end of the drying and deoxidizing chamber by gravity. Preferably, vthe bri-- quettes are discharged from the press onto a grizzly over which they pass by gravity to the forwarder charging end ofthe traveling hearth? The traveling hearth then .extends continuously through the drying, deoxidizing, `and reducing chamber or chambers of the apparatus. With such an arrangement of apparatus, the agglomerates are subjected t0 the minimum amount of 'handling and. disturbance, and little, and frequently no, bond- 60, ing agencies are necessary. The fines in the ore and coal, the intimate mixing and the briquetting pressure are often 'sufficient to form agglomerates that will'hold together dui-ing their passage through the drying, deoxidizing and reducing. chambers where the only strains the agglomerates encounter are those of decrepitation or disruption of an ag-4 glomerate from within as water vapor, reduction gases and zinc vapor are evolved therefrom. l

When bituminous or caking coalis used as the reducing agent, the front extension of the traveling hearth may advantageously be used to support the agglomerates during a caking and deoxidizing operation. Thus, the porous charge of agglomerates supported on a traveling hearth, and preferably on a bed of fines carried by atraveling conveyor, ad.-

vances first through a caking and dcoxid'izing vchamber and then througha reducing chamber. The caking and deoxidizing temperatures and the time 'of calring and deoxidizing are synchronized with the reducing operation so that the agglomerates will Abe appropriately calred, and deoxidized as they leave the caking and deoxidizing chamber and enter the reducing chamber.

The aforementioned and other novel features of the invention will be best understood from thefollowing description taken in conjunction with the accompanying drawings, in which Fig. 1 is a top plan viewof the improved zinc smelting apparatus of the invention.v

Fig. 2 is a longitudinal sectional elevation on the section line 2-2 of Fig. 1

Fig. 3 is a transverse4 sectional elevation on the section-lineB-- of Fig. 1.

Fig. 4 is a vtransverse sectional elevation on the section line 4-4 of Fig. 1-.

Fig. 5 is a longitudinal sectional elevation of the recuperator on the section line 5-5 of Fig. 1.

Fig. 6 is a diagrammatic top plan view of a Vslightly modified form of apparatus, and Fig. 7 is a detail sectional elevation of the charging end of the apparatus of Fig. 6.

The apparatus illustrated inthe drawings comprises a` substantiall"` horizontal reducing chamber 10 embodiel "in an appropriate furnace structure 11 having a'lieating iiue 12 overlying the roof or arch 13 of the reducing chamber. L Gas ports 14;; and V- 15 extend through the side wall of the furnace structure and. conduct preheated air and fuel gas,

respectively, from a recuperator 16 to the flue y 12 where these gases are burned and the re sulting hot products of combustion flow through the flue to a gas outlet 17 communieating with the recuperator.

v The recuperator is built alongside the charging end of the furnace Air is supplied to the recuperator through a pipe 18 communicating with a longitudinal distributing duct 19 in the bottom of the recuperator. The air is distributed from-the duct 19 to. a multiplicity of vertical passages or conduits 20. Similarly, fuel gas is slpplied through a pipe 21 to a distributing 'uct 22 and thence to a multiplicity of vertical passages6 or conappropriate clean-out openings (not shown) duits 23. The passages 2O and 23 are provided in a plurality (six in the apparatus indicated) of spaced vertical walls built up of temperature-resistant brick, tile, or the like. The vertical passages 20 and 23 communicate at their tops with longitudinal ducts 24 and 25, respectively, which in turn communicate with the ports 14 and 15, respectively.

The recuperator is provided with staggered horizontal balles 26 which cause the heating gases delivered from the gas outlet 17 of the heating flue 12 to follow a zig-zag path in their flow through the recuperator to a gas outlet 27 and communicating stack 28. The rccuperator will be further provided with for the various gas passages thereof.

The bottom of the reducing chamber 10 is formed by a traveling hearth which in the apparatus of the drawings comprises a pan conveyor 30 carrying a bed of fines 31. In its passage through the reducing chamber the conveyor is supported on each side by flanged rollers 32 running 0n rails 33, and by intermediate rollers 34 running on rails 35. It will be understood, of course, that the rollers 32 and 34 are appropriately spaced longituamined. Dust from the discharging residues dinally to support the weight of the charge carried by the pan conveyor. At its ends the pan conveyor passes around appropriate guiding and/or driving wheels 36 as will be well understood by those skilled in the art.

At the charging end of the furnace a fines hopper 37, a spent agglomerate hopper 38 and a fresh agglomerate hopper 39 are arranged side by side, the agglomerate hoppers 38 and 39 being provided with mechanical sealing bells 40. The residue discharge end of the furnace is partially enclosed by a casing 41, provided with an end-door 42, normally open through which the discharge end of the moving hearth may be conveniently exis for the most part drawn into a stack 43.

A gas outlet 44 communicates with the top of the reducing chamber 10 near the charging end thereof. The outlet 44 extends transversely across substantially the entire width of the reducing chamber and projects upwardly through the flue 12 and the overlying layers of heat refractory material. Near its upper end, the outlet 44 communicates with two gas off-takes 45 operatively connected to condensers. Above the furnace structure, the outlet 44 is surrounded by a mass of dust coal 46 appropriately confined by the con?,

denser structures and a sheet metal wall 47. A pressure responsive device 48 is inserted in the top of the outlet 44 and is operatively connected to a pressure gaugc'49 and a pres- 'sure recording instrument 50. The condcnsers connected to the off-takes 45 are of the multi-channeled type described in the copending patent application of Frank G. Breyer, Ser. No. 167 ,135, filed February 10, 1927. Each condenser comprises a gas distributing and molten metal collecting chamber 51 having a gas inlet in communication with its respective gas oil-take 45. The chamber' 51 is formed in a solid block of carbon and is substantially circular in horizontal section, and is covered on top byY graphiteblocks 52 in which a multiplicity'ol holes 53 are bored in concentric circles. A multitubular condensing tower is mounted on the graphiteblocks 52 with its multi plieity of upright tubes or channels 54 in communication with the holes 53. The tubes 54 are graphite or carbon tubes of about one to three inches internal diameter, having their lower ends seated in appropriate recesses in the top of the graphite blocks 52. The spaces between the tubes 54 are filled with hardened carbon paste 55. The tower and carbon block (torming the chamber 51) are surrounded by a mass of dust coal 56 appropriately confined by a metal casing 57. The entire condenser structure is mounted on wheels or trucks 58 supported on top of the furnace structure. The condensers are thus conveniently moved into and away from their operative positions with respect to the gas off-takes 45.

A sheet metal hood 59 covers the tops or gas eXit ends of all the channels 54. The lower edge or rim of the hood 59 is embedded to a desired extent in the surrounding dust coal 56. The hood has a top opening in which a vertically disposed exhaust pipe 60 is operatively inserted. The pipe 60 has agate or other appropriate valve 61. A pressure responsive device 48 is inserted within the hood 59 and is operatively connected to a pressure gauge 49 and a pressure recording instrument 50.

The chamber 51 is provided near its bottom and opposite its gas inlet with a tap hole 62 through which molten zinc metal may be withdrawn from the chamber from time to time. The tap hole 62 is normally closed by an inner graphite plug 63 secured to a manipulating -rod 64 and an outer plug 65 of ire clay or the like. rlhe chamber 51 is also provided with a clean-out opening 6G, normally sealed, substantially opposite its gas inlet. Normally, the openings in the condenser structure into which the outer ends of the tap hole 62 and clean-out opening (i6 extend are closed with caps 67 ot graphite or other appropriate material.

The furnace illustrated in the drawings is provided with two additional condensers, making four in all. The additional condensers are of the same type and construction as those already described and are connected to gas olf-takes 68 communicating with the reducing chamber 10 through appropriate ilues in the side walls of the chamber. The olf-takes 68 are positioned at any appropriate distance from the outlet 44, and above the furnace structure 11 are appropriately invthrown between the oit-takes 68 and the eondensers, after the latter have been placed in their respective operating positions. @rdinarily, the distance between the oit-takes 68 and the outlet 44 will be approximately one-third the total length of the furnace.'

ln practicing our presentinvention in the apparatus illustrated in the drawings, we preferably conduct the operations in accordance with the principles described in our aforementioned copending application. rthe pan conveyors as they enter the reducing chamber traveling in the direction indicated by the arrow (F 2) `arecovered with an appropriate layer of [ine material delivered onto the pans from the hopper 37. ifiorlred-v oii' orspent agglomerates are delivered onto the bed ot fines from the hopper 38 and become partially embedded in the iines and to this extent prevent the embedding ot the agglomerates undergoing reduction. |The bed of iines should be of a dept-h adapted to cush ion the `agglomerates against objectionable jarring as the pan conveyor travels through the reducing chamber l0.V vrUnless the agglomerates are gently moved through the chamber, they will tend to be iostledagainst one'another and thus settle into a compact mass that is not conducive to a free ilow of gases through the voids normally present in an agglomerated charge. lThe agglomeration of the mixed charge, includkving the size, shape, strength and manner ot' making the aggloi'nerates as well as the progression of the agglouierates through the reducing chamber,4 are conducted with the view of securing the optimum conditions for the rapid transfer of heat through the agglomerated charge by rcurrents of hot gases. rl`he agglomerat'ed 'charge is delivered from the hopper 39 onto the layer (approximatelyv one agglomerato deep) of spent agglomerates. 'lhe layer of spent agglomerates interposed between the bed-ot ines and the overlying layer of agglomeratesfiindergoing reduction insuresthe desired porosity of the entire bed 'of these latter agglomerates, and, consequently,'the eflicient transfeiyof heat by currents of hot gases throughout the bed of these agglomerates. The layer of agglomerates comprising the charge proper is of a depth adapted to avoid crumbling of the lowermost agglomerates by the overhead ag glomerates. The spent residues and ines are discharged from` the pan conveyor onto a grizzlyO through which the fines pass while the agglomerates slide down the. grizzly and are appropriately disposed of. The ii'ne material passing through the grizzly, is conveyed back to the lines hopper 37 in such amount as required, and an appropriate amount of the spent or worked-oit agglomerates is conveyed back to the hopper 38.

The reducing chamber l0 of the furnace Nillustrated in the drawings is approximately 12 feet wide and 6G feet long. The heating of the reducing chznnber is controlled by maintaining atemperature of about 1300 to 1400o C. in the heating iiue 12 approximate the charging end of the furnace and a teniperature ot about'lQOO" C. in this due approximate th discharging end ot the `i'urnace. The be I of iines is approximately 6 to 9 inches deep and the agglonierated charge near the center of the arch is approxiniately l5 to 18 inches deep. Approximately 30 tons of aggloiinerates will be charged to the furnace per 2st hours. rEhe spent agglomerates or worlied-otifviesidues are preferably dise charged from the reducing chamber with an average zinc content not exceeding about six per cent, and under favorable conditions of operation this igure may be substantialiy reduced0 The agglomerated charge substantially fil/ls the reducing chamber abovefthe hed ot fines and interposed layer of: spent agglomerates and is progressively advanced through the' chamber by the movement of the pan conveyor. |lihe mixture of metallic zinc vapor and carbon monoxide gas (resulting from the reduction oi' the Zinciiferous material inthe a ggloinerated charge) passes trom the reducing chamber through the gas outlets e and 68 into the four multi-channeled condensers on top of the furnace structure. Substantially all ot' the zinc vapor may be condensed to molten Zinc metal in these eondensers. in actual practice we aim to condense at least 90% oi the zinc vapor as zinc metal, the remainder of the zinc vapor being condensed as blue powder or burned to zinc oxide, both ot which products may be recovered by appropriate means. From time to time, molten zinc metal is withdrawn Jtroni the condensers through their tap holes.

ln the working oft ot the agglomerated charge, 'the zinc compounds in the ore (or other zinciferous material) are reduced to metallic Zinc when the carbon in the carbonaceous reducing agent combines with the oxygen of the zinc/compounds; rllhe ,resulting metallic zinc vapor and carbon monoxide gas constitute the gaseous products of the reduction, and it is the iiow of these gases from their points of generation in the charge through the agglomerates towards the gas outlet of the reducing chamber that provides the medium for the effective transfer of lr'eat from the hot product issuing from the reducing 'chamber A contains metallic zinc va or capable of being directly and economical y condensed to zine metal. By directly condensible to zinc metal we mean that if thekgaseous product is conducted v directly (andwithout intermediate treatment) from the reducing chamber into one or more eondensers' of the present spelter retort furnacetype, at least ofthe metallic zinc vapor in the gaseous product will be condensed as zinc metal. By economically condensible to zinc metal we mean the conl densation `to zinc metal of at least 60% of the metallic zinc vapor in the gaseous product with a reasonable number ofcondensersof the present spelter retort type per ,ton of metal condensed in a given time. It is to be under-l stood, of course, that this language is used merely to describe the qualities of the gaseous product, and is not intended to necessarily mean that the metallic zin'c vapor is, in practicing the\ invention, actually condensed to zinc metal. For, as .previously stated, the metallic zinc vapor contained in the gaseous product issuing from the reducing chamber may, if desired, be condensed as 'zinc dust or blue powder, or burned or,oxidized to pig- Yment zinc oxide, where it is desired tomanufacture these zinc products rather than zinc metal or spelter. .x

In Figs. 6 and 7 oflthe drawings, we have illustrated an arrangement of apparatus for conduct-ing the drying, caking, deoxidizing or other preliminary heat treatment ofthe agglomerates while supported on the same traveling hearth that conveys the agglomerates through the reducing chamber. The furnace structure is extended, vat the charging end; to provide, in effect, prolongations 10 and 12 of the reducing chamberlO and heat- 4 ing flue 12, respectively. The pan conveyor is similarly lengthened lto extend through the chambers 10 and 10. The exhaust gases from the recuperator 16 are conducted by a pipe 72 to the heating flue 12. The gas-outlet 44, extending across thel entire width of the heating iue, constitutes a partition orbulki head between the lues 12 and 12.

A briquetting press 74 is' mounted (adjacent the charging end of the furnace at a suiiicient elevation to enable the briquets to pass into the chamber 1.0 largely by the action of gravity. Thus, the briquets drop from the forming rolls onto a conveyor' 75 that conducts 'i them'to anl inclined grizzly 76. The briquets slide down the grizzly 76 over a' chute 77 onto t-he layer of' spent agglomerates (charged from the hopper 38) overlying the bed of drying or heatiiig the briquets .as they slide downy the grizzly. The material passing through the grizzly 76 falls through a conduit 80 and is appropriately disposed of. A stack 81 communicates with the flue 12 for conveying away the exhaust heating gases. i

The operationv of the apparatus illustrated in Figs. 6 and 7 'will be understood from the foregoing (description. The porous charge of aggloinerates is conveyed vthrough the preliminary heat treatment chamber and the reducing chamber while supported` on a traveling hearth and under conditions avoiding substantially. relative movement of individual agglomerates. In the chamber 10 the agglomerates are subjected to the desired drying, caking, deoxidizing o r other treatment operation, and are then advanced directly into the reducing chamber 10.

`The reducing chamber is relatively long iin the direction of charge' progression and of a substantial width. Thedimensions we have hereinbefore mentioned, 60 feet long and 12 feet wide, are illustrative, but are not Atobe considered as limiting the' application of the invention. In some Cases it will be' end. Such antinclination assists, by the action of gravity, the lmovement-oit' the pan conveyor and its supported l charge through the chamber, and where tlie capacity of the l i reducing chamber is relatively large a substantial economy in power consumption is thereby eii'ected. A

We claim:

1. The method of .reducing zinciierous materials, which comprises progressively passing a porou'scharge of agglomerates of mixed zinciferous and reducing materials through a substantially horizontal and externally heated reducing chamber, said charge of -agglomerates beingI 'supportedon a bediof` fines carried by a traveling conveyor.

with a layer of coarsepmaterial disposed inter-mediate the bed of fines and the charge of agglomerates, heating the agglomerates in iio the course offtheir passage through said chamber to a suiciently high temperature to reduce the compounds of zinc and volatilize the resulting metallic zinc, and withdrawing 2 a 'gaseous product containing' metallic zinc vapor from the reducing chamber.

2;- The method of reducing zinciferous materials, which comprises progressively passing a porous charge'of zinciferous and reduc,-

ing materials through a substantially horil zontal and externally heated reducing chamber, said charge being supported in its passage through said chamber upon a bed 'of nlinescarried by a traveling conveyor with a layer of coarse' material disposed intermediate the lines and the charge, heating said charge in the course of lits passage through said chamber to a suihciently high temperature to reduce the compounds of zinc and 1volatilize fthe resulting metallic zinc, the transfer` of heat from the heated Wall 'of the 5 reducing chamber through the charge being Y e'ectedin large partyx by currents of hot gases generated! Within the charge and flowing through the voids thereotwtowardsthe gas outlet of the'reducing chamber, and Withdrawing from the rediiing chamber a gaseous product containing metallic YZinc vapor. l 3. An apparatus for reducing zinciferous material comprising a relatively long and substantially lhorizontal reducing chamber,' i5 a heating ilue overlaying the top of said chamber, a movable hearth adapted to convey a charge of agglomerates under conditions substantially avoiding relative move- 'ment'ot individual agglomerates through said chamber,- a gas oli-take communicating with said chamber and extending upwardly through said Hue, and a condenser operatively associa ed with said gas oli-take.

4. An :lpparatus for reducing zinciferous l material comprising a relatively long and substantially horizontal reducing chamber, a pan conveyor adapted to move a charge of agglomerates under conditions substantially Iavoiding relative movement of individual agglomerates through said chamber and forming in effect the bottom thereof, a heating flue overlaying the top otfsaid chamber.,

and a gas ofi-take communicating With said chamber and extending upwardly through said line.'

5. An apparatus for reducing'zinciferous material comprising a relatively longand substantially horizontal reducing chamber, a pan conveyor adapted to move a charge of 4o agglomerates under conditions substantially avoiding relative movement ot individual agglomeiates through said chamber and forming in eect the bottom thereof, means :tor covering `said conveyorwith a bed of fines, means for introducing the charge to be reduced upon said bed et lines, a. heating flue overlaying the top oit said chamber, and a gas ov-ta'le communicating with said chainber @and extending. upwardly through said tlue.-

6. An apparatus for reducing ziiiciterous material comprising a substantially7 horizontal preliminary heat-treatment chamber and a substantially horizontal reducing chainbei,

5,5 a movable hearth adapted to convey a charge through said `heata-treatment chamber and through said reducing chamber, means for externally 'heating said reducing `chamber, and means tor withdrawing from said re- 60 ducing chamber the gaseous products generated therein. 1, 'i'. An apparatus for reducing zincifeious material comprising a substantiallyhorizontal preliminary heat-treatment chamber and a suligtantially horizontal reducing chamber,

al pan conveyo^r adapted to vmove through said chambers and forming in effect the bottoms thereof, means for covering'said conveyor With a' bed of lfines, meansfor intro.

ducing the .charge to be treated upon said bed'ot fines, means for externally heating said reducing chamber, and means -lor u-'ithdi'awing from said reducing chamber the gaseous products generated therein.

' 8. .An apparatus for reducing zinciferous material comprising a substantially horizontal preliminary heat-treatment chamber and a substantially horizontal reducing chamber, a movable hearth adapted to convey a charge through saidl heat-treatment chamber and through said reducing chamber, means :tor`

externally` heating saidv reducing chamber, a

recuperator operatively associated With the heating means for said reducing chamber,

means for utilizing the exhaust gases from ment chamber, and means for withdrawing u cts generated therein. g I. 9.- 'lhe method of reducingl zinciterous materials Which comprises passing a porous .charge of agglomerates of mixed zinciferous and reducing materials through a substantially horizontal and externally heated reducing. chamber pvithout substantial breaking7 down of the agglomerates during their eirtire passage through the chamber and-under conditions substantially avoiding relative movement of individual agglomerates, said charge of Yagglomera-tes being spread out in the form ot a layer having a depth adapted to avoid crumbling of' the lo'Wermost agglomerates by the overhead agglomerates,'the aglglomefates being conducted through the chamber Witha 'gentle movement adapted to avoidA ob]ectionable ]arring andjpabrading of the agglomerates, heating the agglomerates --.,the recuperator for heating said heat-treat- Y from said reducing chamberthe gaseous prod- I ico I in the course ot suoli passage to a sutliciently high temperature rto reduce the compounds of zinc and volatilize the resulting metallic zinc, the transfer of heat from the heated Wall of Athe reducing chamber through the charge being eected'in large part by currents or" hot 'gases generated Within the charge and 'owing through the voids thereof toivards the gas-outlet of thereducing chamber, and Withdrawing a gaseous product containing metal- `substantially avoiding relative movement of individual agglomerates, said charge of agiio glomeratesbeing spread out in the form of\` a layer having a depth adapted to avoid' of such passage to a sui'iicientl y high temperavturc to reduce the' compounds of ZincV and volatilize the resulting metallic i zinc, the transfer otheat from the heated wall Vof the reducing chamber through the charge being cectedin large part by currents of hot gases generated within the charge and flowing through the voids thereo towards the gas outlet of the reducing chamber, :and withdrawing a gaseous product containing metallic Zinc vapor from the reducing chamber.

11. The method of reducing zinciferous materials which comprises passing a porous charge of agglomerates of mixedzinciferous and reducing materials supported upon a bed of fines carried by a travelling Aconveyor through a substantially horizontal and exter nally heated reducing chamber without substantial breaking down of the agglomerates during their entire passage through the chamber and @nder conditions substantially avoiding relative movement .of individual.

agglomerates, the bed oh fines being adapted to cushion the agglomerates against the 'arring movement of the traveling conveylyor, said charge of agglomerates being spread out in the form of a layer having a depth adapted s to avoid crumbling of the loWermost agglomerates by the overhead agglomerates, the agglomerates being V conducted through the chamber with a gentle movement Vadapted to avoid objectionable jarring and abrading of the agglomerates, heating the agglomerates lin the course of such passage to a suliciently high temperature' to reduce the compoundstof zinc and volatilize the resulting metallic Zinc,-

the transfer of heat from the heated wall of the reducing -cliamberthrough the charge being effected in large part by currents of hot gases generated within the charge and flowing through the voids thereof towards the gas outlet of the reducing, chamber, and withdrawing a gaseous product containing metallic zinc vapor from the reducing chamber.

12. The method of reducing zinciferous material which comprises progressively passing a porous charge ofagglomerates of mixed zinciferous and reducing materials through a f substantially orizontal preliminary heating chamber a d a substantially horizontal and externally heated reducing chamber,

without substantial breaking down of the ag- `crumbling of the lowermost agglomerate's by the overhead agglomerates, the agglomeraties being conducted through said chambers with a gentle movement adapted to avoid jarring and abrading of the agglomerates, subjecting the agglomerates 1n the course of their passage through the heating chamber to a,

preliminary heating operation, heating the agglomerates in the course of their passage` through the reducing chamber to a suiiciently high temperature to reduce the compoundspf zinc and volatilize the resulting metallic zinc, the transfer of heat from' the heated walls of the reducing chamber throuoh the charge being effected in large part by currents of hot gases generated within the charge and flowing through the voids thereof towards the gas outlet of the reducing chamber, and Vwithdrawing the gaseous product containing metallic zinc vapor from the reducing chamber.

In testlmony whereof we' aiix our signatures. y

FRANK G.. BREYER.

EARL H BUNCE. 

